CN205634946U - Material thermolysis divides reason device - Google Patents

Material thermolysis divides reason device Download PDF

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Publication number
CN205634946U
CN205634946U CN201620022569.2U CN201620022569U CN205634946U CN 205634946 U CN205634946 U CN 205634946U CN 201620022569 U CN201620022569 U CN 201620022569U CN 205634946 U CN205634946 U CN 205634946U
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heat
conducting medium
argument
sub
outlet
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赖正平
沈建民
孙世杰
黄诃
孙幸昕
赖厚安
肖俊勇
石雄伟
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/85—Food storage or conservation, e.g. cooling or drying

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Abstract

The utility model discloses a material thermolysis divides reason device, the device comprises hot decomposition system, material branch reason system, waste heat utilization emission processing system, heating system, steam generation system. The invention advantage is: 1. Fog spouts and takes place the air explosion steam raising in formula steam engine and the steam engine into spouting to explode, controls steam temperature with the interior heat transfer medium's of pipe temperature and has solved state and the increasing the heat efficiency of traditional boiler temperature by carrying high pressure and obtaining steam temperature. 2. Solve heat energy production was used in traditional distillation, evaporation, mummification, extraction etc. Technology energy consumption, speed, manpower, the difficult problem of material separation, adopt steam head -on collision material to obtain the thermolysis, according to the material mass go on branch reason collect have the high efficiency, quick, the mode is novel, the material decomposes in the complete concrete application of reason can be in the decomposition of materials such as sewage, refuse treatment, vegetables processing collection, distillation, concentration, extraction, mummification, the technology of going on with the heat exchange such as refine.

Description

Material thermal decomposition sub-argument device
Technical field
This utility model belong to material concentration, distillation, mummification, extract, refinement field, specifically material heat is divided Solve sub-argument device.
Background technology
Along with in industrial development to material concentration, distillation, mummification, extract, the requirement refined the most rapidly is sent out Concentration, distillation, mummification, extraction, refining equipment are had higher requirement by exhibition, traditional concentration, steaming Evaporate, mummification, extraction, refining equipment complex process, equipment heaviness volume is big, and cost of investment is high, manpower is many, Power consumption height.The most not adapting to the needs of current industrialized great production, this utility model is at original sun Can oil heat conducting and supplying device, Thermal-radiation internal-circulationpower power generation device, the decomposition of multipurpose spraying-exploding type high-pressure tempered gas Upgrading is improved on dry type steam generator.The steam produced in former dry type steam generator is with various Water transform in material after head-on collision, is gas within material vapors decomposes coil pipe by material, enters spray quick-fried also Former room, the distance aloft floated is with more different than the position of resedimentation, and the result that it obtains is different, decomposable asymmetric choice net Any material, and water becomes the distance role farthest after steam cooling is reduced.Due to design reduction room Simple in construction, thermally decompose imperfect, material sub-argument is unintelligible, UTILIZATION OF VESIDUAL HEAT IN and emission are collected the most not Can apply the technique with some requirements at the higher level, this utility model not only improves on some original equipment And with the addition of thermal decomposition system, hot sub-argument system, UTILIZATION OF VESIDUAL HEAT IN emission collection system, enable devices to fill Point carry out substance decomposition and implement all kinds of material sub-argument and UTILIZATION OF VESIDUAL HEAT IN emission and collect and meet various technique Requirement and reached zero-emission, especially to offal treatment is refined the sub-argument and medicine that wherein may utilize material Industry technique is distilled, extract various materials etc. have material segmentation collect industry can reach classification segmentation receive The effect of collection.Its advantage is that the thermal decomposition system in material thermal decomposition, sub-argument device can make material divide in heat Solution preocess expands mummification material suddenly and is kept completely separate and is formed expansive force and material has heat wanting to cold flight Ask and make material to rotating the flight of sub-argument tower front end；Quality according to different material collects under conditions of different temperatures Poly-rule, the rotation sub-argument tower in hot sub-argument system uses different temperature to be adjusted the material after separating Different product collecting tanks is entered according to material quality difference own；In UTILIZATION OF VESIDUAL HEAT IN emission collection system After collecting product under the condensation of condensing unit, waste heat can sufficiently be collected adjustment by bootstrap system Send into after temperature and use end, emission system in running to devise desulfurization and emission collection system Enter the material sub-argument tower in device after the collection of emission to carry out process and reach zero-emission.
Utility model content
In order to solve commercial production concentrates, distill, mummification, extraction, refining technique energy consumption is big, investment The state this utility model such as cost height, extraction process time length, material classification sub-argument are unintelligible provide a kind of mould Formula novelty, simple structure, energy-efficient, thermal conversion efficiency is high, heat exchange area is abundant, material classification is complete, Decompose fully, sub-argument is clear, gathering speed is fast, simple operation, UTILIZATION OF VESIDUAL HEAT IN, divide without the material heat discharged Solve sub-argument device.
This utility model solves the technical scheme of above-mentioned technical problem:
Material thermal decomposition sub-argument device is by thermally decomposing system, material sub-argument system, UTILIZATION OF VESIDUAL HEAT IN emissions processes System, heating system, steam generating system form.
1) thermal decomposition system:
1) structure of thermal decomposition system:
Described thermal decomposition system by heat-conducting medium pipe, material thermal decomposition pipe, liquid feedstock tank, feeding-in solid body tank, Solid Conveying and Melting device, liquid feed pipe and feeding-in solid body pipe composition.
Described heat-conducting medium pipe and material thermal decomposition pipe are double-tube heat exchanger, are externally provided with heat-insulation layer, overlap outer tube layer For heat-conducting medium pipe, internal layer is material thermal decomposition pipe；Being heat-conducting medium in described heat-conducting medium pipe, heat conduction is situated between Matter is conduction oil or fuse salt；It is mixed material to be thermally decomposed and steam in described material thermal decomposition pipe.
Described liquid feedstock tank is slack tank body, the built-in liquid material that need to decompose.
Described feeding-in solid body tank is slack tank body, the built-in solid particle material that need to decompose.
2) annexation of thermal decomposition various parts:
Gas-distributing cylinder is connected with the A12 end of jet chimney, the B12 end of jet chimney and liquid feedstock tank and solid The outlet of carrier connects, and is connected with the import of material thermal decomposition pipe at the B12 end of jet chimney the most again, The import of Solid Conveying and Melting device is connected with the outlet of feeding-in solid body tank, and liquid feedstock is installed in liquid feedstock tank front end Pipe, feeding-in solid body pipe, the outlet of material thermal decomposition pipe and mixed material outlet are installed in feeding-in solid body tank front end The A1 in road connects.
Described heat-conducting medium pipe import is connected with the B13 end of heat-conducting medium conduit, heat-conducting medium pipe outlet with The A14 end of heat-conducting medium outlet conduit connects, and heat-conducting medium outlet conduit is existed by heat-conducting medium circulating pump B14 end is connected with the heating coil of heating system constant temperature oven.
2) material sub-argument system:
1) structure of material sub-argument system:
The structure of described material sub-argument system rotates sub-argument tower or horizontal sub-argument device composition.
1.1) described rotation sub-argument tower bottom is in funnel shaped rotary tank, has particulate matter at rotary tank
Product collecting tank, more than tower bottom in cylindrical shape, tower wall more than tower inner bottom part is from bottom to up The multiple structure that repeats, it is uniformly provided with convection current water interlayer, is arranged above with overflow pipe at convection current water interlayer, In the middle of tower, every layer of convection current water interlayer is arranged over deflection plate, and tower outer wall is provided with cooling water layer, the first cooling water layer Inside being provided with condensate water guide sheet, tower top is respectively equipped with the first explosion proof door and the first inspection manhole, in outer every layer of tower The lower section of convection current water interlayer position is provided with the first product collecting tank.
1.2) described formula horizontal sub-argument device is bullet, pre-small post-large, and device inwall is equipped with dividing plate, outside
There is cooling water flow deflector in having the second cooling water layer, cooling water layer, the second product is installed below device Collecting tank, tail end are provided with the second explosion proof door and the second inspection manhole.
1.3) the first mixed material outlet subtube and the second mixed material in the hot sub-argument system described in go out Mouth subtube is two constant section ducts that mixed material outlet conduit separates, and the first mixed material outlet is in charge of First valve is installed on road, the second mixed material outlet subtube is provided with the second valve, the first valve Play with the second valve according to combustion different and select horizontal sub-argument device or rotate sub-argument tower carry out thing The effect of material sub-argument.
2) annexation of material sub-argument various parts:
2.1) inlet tube and first of the cooling water layer of described rotation sub-argument tower cools down the B3 end that water water inlet is in charge of
Connecting, the outlet and first of the first cooling water layer rotating sub-argument tower cools down the A6 that water backwater is in charge of End connects；The import rotating sub-argument tower is connected with the B1 end of mixed material outlet conduit.
2.2) inlet tube and second of the cooling water layer of described horizontal sub-argument device cools down the B4 that water water inlet is in charge of End connects, and the A7 end that the outlet of the cooling water layer of horizontal sub-argument device and the second cooling water backwater are in charge of is even Connect；The import of horizontal sub-argument device is connected with the B2 end of mixed material outlet conduit.
3. UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
1) structure of UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
Described UTILIZATION OF VESIDUAL HEAT IN emission treatment systems is mainly by cooling tower, cooling tower water inlet pipe, hot water swap tank Form with desulfation dust-extraction device.
Described cooling tower is slack tank body；Described hot water swap tank is slack tank body, the built-in water of tank
And it is provided with waste heat coil pipe.
2) annexation of each parts of UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
Described cooling tower is connected with hot water swap tank by conducting water inlet pipe, and the A15 end of conducting water inlet pipe is with cold
But the import of tower connects, and the B15 end of conducting water inlet pipe is connected with the import of hot water swap tank；Cooling tower The water inlet outlet company by the first cooling B7 end of being in charge of of water backwater and A6 end with the first cooling water layer Connecing, the outlet of cooling tower is intake with the first cooling water respectively by cooling water circulating pump and cooling water inlet pipe The B3 end being in charge of and the second cooling water B4 end of being in charge of of water inlet are cold with the first water inlet cooling down water layer and second But water layer water inlet connects.
Described waste heat coil pipe lower end is connected with the flue outlet of heating system；Described waste heat coil outlets and desulfurization The import of dust arrester connects, and the outlet of desulfation dust-extraction device is connected with the import of air-introduced machine；Desulfurization and dedusting fills The water inlet put is connected with water inlet pipe, the mixture outlet of desulfation dust-extraction device passes through blow-off pipe and liquid feedstock The import of tank connects.
4. heating system:
1) structure of heating system:
Described heating system is logical by constant temperature oven, heating coil, cigarette, low level heat-conducting medium storage tank and high-order heat conduction Media expansion groove forms；
Described constant temperature oven is heated at constant temperature body of heater, has heat-insulation layer outside body of heater, interior for heating chamber, sets in heating chamber
There is the heating coil of band heat-conducting medium import and export pipe.
2) annexation of each parts of heating system:
The described high-order outlet of heat-conducting medium expansion slot is connected with the import of low level heat-conducting medium storage tank；Described low The outlet of position heat-conducting medium storage tank is by the B11 end of heat-conducting medium inlet tube and the first of steam generating system Heat-conducting medium layer connects；After the outlet of described heating coil is connected with the A11 end of heat-conducting medium inlet tube and The outlet of low level heat-conducting medium storage tank connects；The import of described heating coil and heat-conducting medium outlet conduit B14 end connects, the outlet of the heat-conducting medium conduit of the A14 end of heat-conducting medium outlet conduit and thermal decomposition system Connect；The import of heat-conducting medium conduit is connected with the outlet of the 8th heat-conducting medium layer of steam generating system；Lead Heat-conducting medium circulating pump is had on thermal medium outlet pipeline.
5. steam generating system
1) structure of steam generating system:
Described steam generating system mainly by high-pressure plunger pump, spraying-exploding type steam engine, high pressure sprays fog equipment, point Cylinder and relief valve composition.
There is the multilamellar ring-type sealing ring road of heat-insulation layer outside described spraying-exploding type steam engine, be the first heat-conducting medium respectively Layer, the second heat-conducting medium layer, the 3rd heat-conducting medium layer, the 4th heat-conducting medium layer, the 5th heat-conducting medium layer, 6th heat-conducting medium layer, the 7th heat-conducting medium layer and the 8th heat-conducting medium layer, the first vapor film, the second steam Layer, the 3rd vapor film, the 4th vapor film, the 5th vapor film, the 6th vapor film and the 7th vapor film, first Vapor film and the second vapor film, the second vapor film and the 3rd vapor film, the 3rd vapor film and the 4th vapor film, 4th vapor film and the 5th vapor film, the 5th vapor film and the 6th vapor film, the 6th vapor film and the 7th steam Layer is respectively equipped with communicating pipe, the first heat-conducting medium layer and the second heat-conducting medium layer, the second heat-conducting medium layer and the Three heat-conducting medium layers, the 3rd heat-conducting medium layer and the 4th heat-conducting medium layer, the 4th heat-conducting medium layer and the 5th are led Thermal medium layer, the 5th heat-conducting medium layer and the 6th heat-conducting medium layer, the 6th heat-conducting medium layer and the 7th heat conduction are situated between Matter layer, the 7th heat-conducting medium layer and the 8th heat-conducting medium layer are respectively equipped with communicating pipe.
2) annexation of each parts of steam generating system:
7th vapor film outlet of the spraying-exploding type steam engine in described steam generating system is exported by vapor film Pipeline is connected with the import of gas-distributing cylinder.
8th heat-conducting medium layer outlet of described spraying-exploding type steam engine is connected with the A13 end of heat-conducting medium conduit.
The outlet of described gas-distributing cylinder is connected with the A12 end of jet chimney, the B12 end of jet chimney and material heat The import decomposing pipe connects；
Described high-pressure plunger pump inlet is connected with the water out of hot water swap tank；High-pressure plunger pump discharge is by height Hydraulic plunger pump outlet is connected with high pressure sprays fog equipment.
On described gas-distributing cylinder, relief valve is installed.
Above-mentioned constant temperature oven is 1～100 constant temperature oven parallel combination body.
Above-mentioned rotation sub-argument tower and horizontal sub-argument device are assemblys that can be jointly in parallel.
More than above-mentioned rotation sub-argument tower interior bottom portion from bottom to up for repeat multiple structure, can be 1～ 100 layers.
It is from first to last the many diaphragm structures repeated inside above-mentioned horizontal sub-argument device, can be 1～100 Block dividing plate.
Advantage of the present utility model:
1. the spraying-exploding type steam engine integrated heat efficiency that the thermal efficiency of material thermal decomposition sub-argument device uses at heat energy 93% can be reached.Due to direct heat transfer, pressure during steam head-on collision substance decomposition, sub-argument, collection Advance, be actively entered, the feature of increment evaporation makes technological process shorten, reduces；The speed of service is accelerated；Heat Exchange area expand (mass expansion makes heat exchange area several times increase) fundamentally change indirect heat exchange, oneself So evaporate, be additionally related to multi-functional passive entry, the heat exchanging process of decrement evaporation, overall efficiency exceedes the 50% of former traditional handicraft Above.Improve the thermal efficiency, save energy consumption.
2. break through the pattern of steaming of upper century-old decocting in water bubble type, carry out spraying air blasting steam by adding streamer, Steam engine heat exchange area makes full use of, and water smoke 1Kg water is in interior diameter 100mm pipe, and its surface area is: 55606mm3；The water droplets of 1 a diameter of 0.1mm, its weight is 4.19 × 10-9Kg, 1Kg water has 2.387×108Individual water droplet.The surface area of each water droplet is 0.1257mm2, total surface area is 3 × 107mm2。
It can be seen that 1Kg water smoke chemical conversion average diameter is the water droplet of 0.1mm, its surface area ratio aqueous water expands Big 539 times.
3. the thermal conversion efficiency of spraying-exploding type steam engine is up to more than 93%, spraying-exploding type steam engine high pressure sprays fog equipment Pressure sprays into steam flow speed and reaches more than 110 kilometers per hour, with heat transfer heat carrier (heat pipe in steam engine) Evaporated conductive, radiation, convection velocity is greatly speeded up after producing air blasting.Improve the thermal efficiency.
4. spraying in quick-fried steam engine thermal conductive pipe is heat-conducting medium, heat-conducting medium have be heated fast, thermal storage time length Feature.
5. there is heat conduction carrier to complete owing to water spray carries out heating vapor (steam) temperature and can arbitrarily adjust temperature, Atomized water spray the quantity of vapour by the quantity and controlling controlling to enter water smoke in a closed cavity can be Produce air pressure in cavity and can control pressure size, such steam engine can reach high pressure low temperature, high pressure-temperature and Low-pressure low-temperature, low-voltage high-temperature improve the safety coefficient of steam engine.
6. it is unique with bushing type adverse current heat exchanger to use, and the circulus of multilamellar provides and sufficiently changes Hot side amasss, and not only heat exchange efficiency is high, and easy access is cleaned.
7. spraying-exploding type steam engine is according to specified standards manufacture, can parallel connection reach to use it according to working condition requirement The purpose that number of units can extend at any time, solving enterprise needs not waste resource during enlarged reproduction；Save enterprise Industry cost.
8. atomized water spray enters thermal conductor and solves the drawback needing to arrange condensed water in conventional boiler, and spraying-exploding type steams Without condensed water, Non-scale in steam turbine, use without blowdown, minimizing artificial treatment incrustation scale and charges for disposing pollutants.With saving Water resource.
9. material thermal decomposition sub-argument device for for material drying process because be with steam head-on collision material divide Solve makes moisture content fast vaporizing in material, makes the rapid mummification of solid material；Relatively conventional drying process has speed Spend fast feature, improve the productivity.
10. material thermal decomposition sub-argument device is for can be sleeping when needing to obtain part is useful in material material Formula sub-argument device uses the different requirement difference to temperature of quality of material kissing with it in rotating sub-argument tower The product collecting tank closed obtains, and reaches the purpose of material segmentation.
11. materials thermally decompose sub-argument devices when separating veterinary antibiotics, plant etc. due to water and solid material Separating, while collection material reaches material application target, the water separated can also recycle, Obtain the water preparation goods of various material.
In 12. material thermal decomposition sub-argument device application processes, waste-heat recovery device is by waste heat recovery, has corrected biography System technique wastes the disadvantage of heat energy in a large number, has reached the purpose of real energy-saving and emission-reduction.
13. material thermal decomposition sub-argument devices in use can accomplish generator fixed fire producing steam at any time, Heat-conducting medium in constant temperature oven and spraying-exploding type steam engine heat-conducting medium pipe can be certainly when temperature reaches technological requirement Dynamic stop and start, have saved the energy.
Heat-conducting medium in heat-conducting medium pipe in constant temperature oven when 14. material thermal decomposition sub-argument devices need not steam There are stronger accumulation of energy effect, heat-conducting medium specific heat can play greatly regulation temperature action, also function to energy-saving and emission-reduction Effect.
The temperature that 15. material thermal decomposition sub-argument devices need according to different materials in implementation process can be controlled Heat in decomposing system that the temperature of heat-conducting medium is to meet the temperature needs of material, with temperature control in other techniques Make difficulty and in order to control and adjust the phenomenon of the temperature waste energy, saved the energy, improve the thermal efficiency
16. materials thermal decomposition sub-argument devices in application process owing to improve the productivity, having saved the energy and make Enterprise reduces production cost, improves the market competitiveness, achieves the bigger profit of enterprise.
17. materials thermal decomposition sub-argument device ranges of application and extensively, due to have concentration, distillation, mummification, The function extract, refined can be at sewage, Treatment of Sludge, domestic rubbish disposal, veterinary antibiotics mummification Reason, veterinary antibiotics natural juice are refined, acid purifications, feed manufacturing, sugared purification processing, ethanol purification processing, Spirit, mineral classification processing, petrochemical industry refinement, Pharmaceutical purification, distillation technique, garbage carry The industrial technique taking nutrient substance, utility etc. is integrated
This utility model is the spraying-exploding type steam engine invented at research pot and the thermal efficiency of stove and research steam The thermal decomposition of invention material, sub-argument device in the technique utilized and use.This product has compared with similar products Having safe and reliable, the life-span is long, and device simple is easy to maintenance, the feature that cost of investment is low.The whole world is always All studying the thermal efficiency how improving body of heater material, the mode of entrance etc. of fuel usually to manufacture, all Pot and stove being come together to talk the thermal efficiency, but have ignored the research individually to pot, this utility model utilizes material to deposit It is that the principle of intermolecular a kind of captivation is studied.For the material that composition is similar with structure, it is right The physicochemical properties such as the boiling point of water, fusing point, heat of gasification, heat of fusion, dissolubility, surface tension, viscosity Difference has the quality of material own and determines, typically strengthens along with the increase of relative molecular mass, so wanting Improve the pot thermal efficiency it is necessary to be pumped with machinery and liquid water become steam fog carry out heating and realize steam
This utility model is investigated the use field of steam, uses heat exchange to extract at multistage evaporation etc. Take, separate, purify, distill, that the technique such as mummification all consumes and waste heat energy is very big, between basic disadvantage is Connect heating, long processing time and consume heat energy and collect different material use multistage collection technique, this practicality Novel employing directly makes material rapid expanding with steam head-on collision material, various element fast decoupleds in material, and Carrying out rapid condensation by rotation sub-argument tower makes various material reach in the gathering of its product collecting tank matched Material classification is complete, decompose the purpose abundant, sub-argument is clear, gathering speed is fast, it is provided that a kind of pattern is new Grain husk, simple structure, energy-efficient, thermal conversion efficiency is high, heat exchange area sufficiently decomposes sub-argument device.
Accompanying drawing explanation
Fig. 1 is that this utility model material thermally decomposes sub-argument apparatus structure schematic diagram.
In figure: thermal decomposition system 1, heat-conducting medium pipe 1-1, material thermal decomposition pipe 1-2, liquid feedstock tank 1-3, feeding-in solid body tank 1-4, Solid Conveying and Melting device 1-5, liquid feed pipe 1-6, feeding-in solid body pipe 1-7.
Material sub-argument system 2, rotate sub-argument tower 2-1, rotary tank 2-1-1, convection current water interlayer 2-1-2, right Overflow pipe 2-1-3, deflection plate 2-1-4, condensate water guide sheet 2-1-5, the first cooling water layer 2-1-6, the One explosion proof door 2-1-7, the first inspection manhole 2-1-8, particulate matter product collecting tank 2-1-9, the first product Collecting tank 2-1-10；Horizontal sub-argument device 2-2, dividing plate 2-2-1, cooling water flow deflector 2-2-2, second Cooling water layer 2-2-3, the second explosion proof door 2-2-4, the second inspection manhole 2-2-5, the second product collecting tank 2-2-6。
UTILIZATION OF VESIDUAL HEAT IN emission treatment systems 3, cooling tower 3-1, cooling tower water inlet pipe 3-2, hot water exchange Tank 3-3, waste heat coil pipe 3-4, air-introduced machine 3-5, hot water swap tank water inlet pipe 3-6, desulfation dust-extraction device 3-7, water inlet pipe 3-8, conducting water inlet pipe 3-9.
Heating system 4, constant temperature oven 4-1, heating coil 4-2, cigarette lead to 4-3, low level heat-conducting medium storage tank 4-4, high-order heat-conducting medium expansion slot 4-5.
Steam generating system 5, high-pressure plunger pump 5-1, high-pressure plunger pump outlet conduit 5-2, spraying-exploding type steam Steam turbine 5-3, high pressure sprays fog equipment 5-4, vapor film outlet conduit 5-20, gas-distributing cylinder 5-21, relief valve 5-22。
Mixed material outlet conduit 6-1, the first mixed material outlet subtube 6-2, the second mixed material go out Mouth subtube 6-3, the first valve 6-4, the second valve 6-5, cooling water inlet pipe 6-6, the first cooling water 6-7 is in charge of in water inlet, 6-8 is in charge of in the second cooling water water inlet, CWR 6-9, the first cooling water return Moisture pipe 6-10, second cooling water backwater be in charge of 6-11, blow-off line 6-16, heating coil 4-2 Heat-conducting medium outlet conduit 6-17, jet chimney 6-18, the heat-conducting medium outlet of spraying-exploding type steam engine 5-3 Pipeline 6-19, the heat-conducting medium inlet tube 6-20 of heating coil 4-2, cooling water circulating pump 7-1, blowdown Pump 7-2, heat-conducting medium circulating pump 7-3.
Fig. 2 is this utility model dry type steam generator A end structure schematic diagram.
Fig. 3 is this utility model dry type steam generator B end structure schematic diagram.
In figure: heat-conducting medium layer 5-5,5-7,5-9,5-11,5-13,5-15,5-17,5-19, steam Vapour layer 5-6,5-8,5-10,5-12,5-14,5-16,5-18, high-pressure plunger pump outlet conduit 5-2, Heat-conducting medium inlet tube 6-17, heat-conducting medium outlet 6-19, vapor film outlet conduit 5-20.
Detailed description of the invention
Material thermally decomposes, sub-argument device embodiments is: the heat conduction being discharged in constant temperature oven by the heat energy of fuel In medium (heat-conducting medium can use conduction oil, fuse salt etc.) and by spraying-exploding type steam engine and thermal decomposition system In heat-conducting medium pipe in heat-conducting medium be heated to the temperature of technological requirement；Water is being sprayed by high-pressure plunger pump Spraying-exploding type steam engine sprays in mist device water smoke, and water smoke produces steam with the acting of heat-conducting medium pipeline.Use Steam power need to material to be processed push thermal decomposition system in thermally decompose；When material enters thermal decomposition Pretreatment need to be carried out, at the heat exchange area calculated between material and thermal decomposition system and pipeline according to different materials After unimpeded factor, heat-conducting medium temperature in thermal decomposition system is adjusted to meet material complete by thermal decomposition system Carry out material decomposition after the temperature of absolutely dryization, during concrete operations, thing can be adjusted by steam valve and feed valves Material admission velocity and quantity of steam meet material mummification, and in thermal decomposition system, the material after thermal decomposition enters rotation Turn sub-argument tower and horizontal sub-argument room, enter and rotate the material solid material of sub-argument tower at particulate matter product collecting tank Collecting, liquid material enters rotation sub-argument tower and carries out the segmentation of material, sub-argument through condensing unit, deflection plate Acting after, enter the first product collecting tank according to the quality of material respectively, enter the thing of horizontal sub-argument device Expecting to be divided into solid-state and liquid to respectively enter through the thermal decomposition of steam Yu material, respective quality adapts second Product collecting tank, carries out waste heat recovery profit entering residual neat recovering system through the rotation condensed water of sub-argument tower With, the flue gas in flue enters waste heat recovery tank dust therein and sulfur respectively enters sedimentation tank and desulfurization dress Put, the dust in sedimentation tank is periodically into rotation sub-argument tower and carries out treatment and purification, and so formation one is complete Technological process without the substance decomposition sub-argument of discharge.
First by steam clean and preheating heat decomposing system and thing every time before enabling material thermal decomposition sub-argument device Matter sub-argument system reaches thermal balance in five minutes；Need after use by steam clean thermal decomposition system and heat Ten minutes cleaning residue remnants of sub-argument system.
Spraying-exploding type steam engine 5-2 can produce low-voltage high-temperature, low-pressure low-temperature, also can high pressure-temperature, high pressure low temperature Steam can also produce superheated steam moment；Use high-temperature steam work done in thermal decomposition system, consider thing Material and thermal decomposition system between heat exchange area and the unimpeded factor of pipeline after by heat-conducting medium in thermal decomposition system 1 Temperature is adjusted to meet material by carrying out material decomposition after the temperature of the complete mummification of thermal decomposition system, horizontal sleeping Formula sub-argument device 2-2 and rotation sub-argument tower 2-1 can use material difference after disassembly according to technological requirement Quality is collected；Waste heat coil pipe 3-4 in UTILIZATION OF VESIDUAL HEAT IN emission treatment systems 3 is by after device warm Waste heat utilizes；Desulfation dust-extraction device 3-7 in UTILIZATION OF VESIDUAL HEAT IN emission treatment systems 3 is by plant running During emission process after the hot sub-argument system 1 that enters in device carry out sub-argument；Define one whole Set material processs, decomposition, heat energy, water circulation use device i.e.: material thermally decompose, sub-argument device.Very Just improve the thermal efficiency of constant temperature oven and various concentration, distillation, mummification, extraction, the speed of refining technique and Efficiency and zero-emission, it is achieved that practical significance energy-saving and emission-reduction.
Below in conjunction with the accompanying drawings and be embodied as this utility model is further described.
Material thermal decomposition sub-argument device burn cycle structure is as it is shown in figure 1, steam head-on collision material thermally decomposes sub-argument Device is by thermally decomposing system 1, material sub-argument system 2, UTILIZATION OF VESIDUAL HEAT IN emission treatment systems 3, heating system System 4, steam generating system 5 form.
1) thermal decomposition system:
1) structure of thermal decomposition system:
Described thermal decomposition system 1 by heat-conducting medium pipe 1-1, material thermal decomposition pipe 1-2, liquid feedstock tank 1-3, Feeding-in solid body tank 1-4, Solid Conveying and Melting device 1-5, liquid feed pipe 1-6 and feeding-in solid body pipe 1-7 composition.
Described heat-conducting medium pipe 1-1 and material thermal decomposition pipe 1-2 is double-tube heat exchanger, is externally provided with heat-insulation layer, Set outer tube layer is heat-conducting medium pipe 1-1, and internal layer is that material thermally decomposes pipe 1-2；Described heat-conducting medium pipe 1-1 Being inside heat-conducting medium, heat-conducting medium is conduction oil or fuse salt；It is to treat heat in described material thermal decomposition pipe 1-2 The mixed material decomposed and steam.
Described liquid feedstock tank 1-3 is slack tank body, the built-in liquid material that need to decompose.
Described feeding-in solid body tank 1-4 is slack tank body, the built-in solid particle material that need to decompose.
2) annexation of thermal decomposition various parts:
The A12 end of gas-distributing cylinder 5-21 and jet chimney 6-18 is connected, the B12 end of jet chimney 6-18 with The outlet of liquid feedstock tank 1-3 and Solid Conveying and Melting device 1-5 connects, the most again at the B12 of jet chimney 6-18 The import with material thermal decomposition pipe 1-2 is held to be connected, the import of Solid Conveying and Melting device 1-5 and feeding-in solid body tank 1-4 Outlet connect, liquid feedstock tank 1-3 front end install liquid feed pipe 1-6, feeding-in solid body tank 1-4 front end Feeding-in solid body pipe 1-7, the outlet of material thermal decomposition pipe 1-2 and the A1 of mixed material outlet conduit 6-1 are installed Connect.
Described heat-conducting medium pipe 1-1 import is connected with the B13 end of heat-conducting medium conduit 6-19, and heat conduction is situated between Matter pipe 1-1 outlet is connected with the A14 end of heat-conducting medium outlet conduit 6-20, heat-conducting medium outlet conduit 6-20 Heating coil by heat-conducting medium circulating pump 7-3 constant temperature oven 4-1 in B14 end with heating system 4 4-2 connects.
2) material sub-argument system:
1) structure of material sub-argument system:
The structure of described material sub-argument system is formed by rotating sub-argument tower 2-1 or horizontal sub-argument device 2-2.
1.1) it is in funnel shaped rotary tank 2-1-1 bottom described rotation sub-argument tower 2-1, at rotary tank
Have particulate matter product collecting tank 2-1-9, more than tower bottom in cylindrical shape, tower inner bottom part with On tower wall from bottom to up for repeat multiple structure, be uniformly provided with convection current water interlayer 2-1-2, to flowing water Interlayer is arranged above with overflow pipe 2-1-3, and in the middle of tower, every layer of convection current water interlayer 2-1-2 is arranged over baffling Plate 2-1-4, tower outer wall is provided with cooling water layer 2-1-6, is provided with condensed water and leads in the first cooling water layer 2-1-6 Flow 2-1-5, tower top is respectively equipped with the first explosion proof door 2-1-7 and the first inspection manhole 2-1-8, outside tower The lower section of every layer of convection current water interlayer 2-1-2 position is provided with the first product collecting tank 2-1-10.
1.2) described formula horizontal sub-argument device 2-2 is bullet, pre-small post-large, device inwall equipped with every
Plate 2-2-1, there is cooling water flow deflector 2-2-2 outside in having the second cooling water layer 2-2-3, cooling water layer, Be provided with the second product collecting tank 2-2-6 below device, tail end is provided with the second explosion proof door 2-2-4 and second Inspection manhole 2-2-5.
1.3) the first mixed material outlet subtube 6-2 and the second mixture in the hot sub-argument system described in Material outlet subtube 6-3 is two constant section ducts that mixed material outlet conduit 6-1 separates, the first mixing First valve 6-4 is installed, on the second mixed material outlet subtube 6-3 on material outlet subtube 6-2 Second valve 6-5, the first valve 6-4 and the second valve 6-5 are installed play according to combustion difference Horizontal sub-argument device 2-2 or rotation sub-argument tower 2-1 is selected to carry out the effect of material sub-argument.
2) annexation of material sub-argument various parts:
2.1) inlet tube and first of the cooling water layer 2-1-6 of described rotation sub-argument tower 2-1 cools down water
Water inlet is in charge of the B3 end of 6-7 and is connected, and rotate sub-argument tower 2-1 first cools down going out of water layer 2-1-6 The A6 end that mouth pipe is in charge of 6-10 with the first cooling water backwater is connected；Rotate sub-argument tower 2-1 import with mix The B1 end of material outlet pipeline 6-1 connects.
2.2) inlet tube and the second cooling water of the cooling water layer 2-2-3 of described horizontal sub-argument device 2-2 is intake The B4 end being in charge of 6-8 connects, the outlet and second of the cooling water layer 2-1-6 of horizontal sub-argument device 2-2 Cooling water backwater is in charge of the A7 end of 6-11 and is connected；The import of horizontal sub-argument device 2-2 exports with mixed material The B2 end of pipeline 6-3 connects.
3. UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
1) structure of UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
Described UTILIZATION OF VESIDUAL HEAT IN emission treatment systems is mainly by cooling tower 3-1, cooling tower water inlet pipe 3-2, warm Water coke slurry tank 3-3 and desulfation dust-extraction device 3-7 composition.
Described cooling tower 3-1 is slack tank body；Described hot water swap tank 3-3 is slack tank body, the built-in water of tank,
And it is provided with waste heat coil pipe 3-4.
2) annexation of each parts of UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
Described cooling tower (3-1) by conducting water inlet pipe (3-9) be connected with hot water swap tank (3-3), turn on into The A15 end of water pipe (3-9) is connected with the import of cooling tower (3-1), conducting water inlet pipe (3-9) B15 end with The import of hot water swap tank (3-3) connects；The water inlet of cooling tower (3-1) passes through CWR (6-9) B7 end be in charge of the A6 end of (6-10) with the first cooling water backwater respectively and the second cooling water backwater is in charge of (6-11) A7 end and the outlet of the first cooling water layer (2-1-6) and second cool down water layer (2-2-3) water outlet Mouth connects；
The outlet of cooling tower (3-1) is by cooling water circulating pump (7-1) and cooling water inlet pipe (6-6) difference It is in charge of the B3 end of (6-7) with the first cooling water water inlet and the B4 end and the of (6-8) is in charge of in the second cooling water water inlet Water inlet and second cooling water layer (2-2-3) water inlet of one cooling water layer (2-1-6) connect；
Described waste heat coil pipe 3-4 lower end exports with the flue 4-3 of heating system 4 and is connected；Described waste heat coil pipe 3-4 outlet is connected with the import of desulfation dust-extraction device 3-7, the outlet of desulfation dust-extraction device 3-7 and air-introduced machine The import of 3-5 connects；The water inlet of desulfation dust-extraction device 3-7 is connected with water inlet pipe 3-8, desulfurization and dedusting dress The mixture outlet putting 3-7 is connected by the import of blow-off pipe 6-16 and liquid feedstock tank 1-3.
4. heating system:
1) structure of heating system:
Described heating system 4 is led to 4-3, low level heat-conducting medium by constant temperature oven 4-1, heating coil 4-2, cigarette Storage tank 4-4 and high-order heat-conducting medium expansion slot 4-5 composition.
Described constant temperature oven 4-1 is heated at constant temperature body of heater, has heat-insulation layer outside body of heater, interior for heating chamber, heating
Indoor are provided with the heating coil 4-2 of band heat-conducting medium import and export pipe.
2) annexation of each parts of heating system:
The outlet of described high-order heat-conducting medium expansion slot 4-5 is with the import of low level heat-conducting medium storage tank 4-4 even Connect；The outlet of described low level heat-conducting medium storage tank 4-4 by the B11 end of heat-conducting medium inlet tube 6-17 with First heat-conducting medium layer 5-5 of steam generating system 5 connects；The outlet of described heating coil 4-2 and heat conduction The A11 end of medium inlet 6-17 is connected with the outlet of low level heat-conducting medium storage tank 4-4 after connecting；Institute The B14 end of the import and heat-conducting medium outlet conduit 6-20 of stating heating coil 4-2 is connected, and heat-conducting medium goes out The A14 end of mouth pipeline 6-20 is connected with the outlet of the heat-conducting medium conduit 1-1 of thermal decomposition system 1；Heat conduction The import of media lines 1-1 is connected with the outlet of the 8th heat-conducting medium layer 5-19 of steam generating system 5； Heat-conducting medium circulating pump 7-3 is had on heat-conducting medium outlet conduit 6-20.
5. steam generating system
1) structure of steam generating system:
Described steam generating system 5 is main by high-pressure plunger pump 5-1, spraying-exploding type steam engine 5-3, high pressure spray Mist device 5-4, gas-distributing cylinder 5-21 and relief valve 5-22 composition.
Spraying-exploding type steam engine structure as shown in Figures 2 and 3, has heat-insulation layer outside described spraying-exploding type steam engine 5-3 Multilamellar ring-type sealing ring road, be respectively the first heat-conducting medium layer 5-5, the second heat-conducting medium layer 5-7, Three heat-conducting medium layer 5-9, the 4th heat-conducting medium layer 5-11, the 5th heat-conducting medium layer 5-13, the 6th heat conduction Dielectric layer 5-15, the 7th heat-conducting medium layer 5-17 and the 8th heat-conducting medium layer 5-19, the first vapor film 5-6, Second vapor film 5-8, the 3rd vapor film 5-10, the 4th vapor film 5-12, the 5th vapor film 5-14, Six vapor film 5-16 and the 7th vapor film 5-18, the first vapor film 5-6 and the second vapor film 5-8, second Vapor film 5-8 and the 3rd vapor film 5-10, the 3rd vapor film 5-10 and the 4th vapor film 5-12, the 4th steaming Vapour layer 5-12 and the 5th vapor film 5-14, the 5th vapor film 5-14 and the 6th vapor film 5-16, the 6th steaming Vapour layer 5-16 and the 7th vapor film 5-18 is respectively equipped with communicating pipe, and the first heat-conducting medium layer 5-5 and second leads Thermal medium layer 5-7, the second heat-conducting medium layer 5-7 and the 3rd heat-conducting medium layer 5-9, the 3rd heat-conducting medium layer 5-9 and the 4th heat-conducting medium layer 5-11, the 4th heat-conducting medium layer 5-11 and the 5th heat-conducting medium layer 5-13, 5th heat-conducting medium layer 5-13 and the 6th heat-conducting medium layer 5-15, the 6th heat-conducting medium layer 5-15 and the 7th Heat-conducting medium layer 5-17, the 7th heat-conducting medium layer 5-17 and the 8th heat-conducting medium layer 5-19 are respectively equipped with even Siphunculus.
2) annexation of each parts of steam generating system:
The 7th vapor film 5-18 outlet of the spraying-exploding type steam engine 5-3 in described steam generating system 5 is passed through The import of vapor film outlet conduit 5-20 and gas-distributing cylinder 5-21 is connected.
The 8th heat-conducting medium layer 5-19 outlet of described spraying-exploding type steam engine 5-3 and heat-conducting medium conduit 6-19 A13 end connect.
The outlet of described gas-distributing cylinder 5-21 is connected with the A12 end of jet chimney 6-18, jet chimney 6-18 The import of B12 end and material thermal decomposition pipe 1-2 be connected.
Described high-pressure plunger pump 5-1 import is connected with the water out of hot water swap tank 3-3；High-pressure plunger pump 5-1 outlet is connected with high pressure sprays fog equipment 5-4 by high-pressure plunger pump discharge pipe 5-2.
On described gas-distributing cylinder 5-21, relief valve 5-22 is installed.
Above-mentioned constant temperature oven 4-1 is 1～100 constant temperature oven parallel combination body.
Above-mentioned rotation sub-argument tower 2-1 and horizontal sub-argument device 2-2 is assembly that can be jointly in parallel.
More than above-mentioned rotation sub-argument tower 2-1 interior bottom portion from bottom to up for the multiple structure repeated, Ke Yishi 1～100 layer.
Inside above-mentioned horizontal sub-argument device 2-2 from first to last for repeat many diaphragm structures, can be 1～ 100 pieces of dividing plates.
When implementing this utility model:
By heat-conducting medium (heat-conducting medium can use conduction oil, fuse salt etc.) injection heating system 4 constant temperature oven The heating coil 4-2 of 4-1, the heat-conducting medium layer of steam generating system 5 spraying-exploding type steam engine 5-3 and heat point In the heat-conducting medium pipe 1-1 of solution system 1, constant temperature oven 4-1 use fuel (as coal dust, fuel oil, combustion gas, Biomass etc.) combustion heating as the kindling material in burner hearth, open heat-conducting medium circulating pump 7-3, make heat conduction be situated between Matter is in heating coil 4-2, the heat-conducting medium layer of spraying-exploding type steam engine 5-3 and the thermal decomposition system of constant temperature oven 4-1 Circulation in the heat-conducting medium pipe 1-1 of system 1, heat-conducting medium is heated to operating temperature, makes spray by constant temperature oven 4-1 Each layer heat-conducting medium layer of quick-fried formula steam engine 5-3 is heated to operating temperature, each layer of spraying-exploding type steam engine 5-3 Heat is delivered heat to each layer vapor film of spraying-exploding type steam engine 5-3 by heat-conducting medium layer；During constant temperature oven 4-1 burning After the flue gas discharged enters flue 4-3, when the waste heat coil pipe 3-4 in superheated water swap tank 3-3, will Water heating in hot water swap tank 3-3；Emission enters the water of desulfation dust-extraction device 3-7 and water inlet pipe 3-8 After mixing, enter liquid feedstock tank 1-3 by dredge pump 7-2 and blow-off line 6-16 and enter thermal decomposition System 1 is to reach emissions processes purpose.By the water in hot water swap tank 3-3 through high-pressure plunger pump 5-1 Outlet made water fogging by high-pressure plunger pump outlet conduit 5-2 and high pressure sprays fog equipment 5-4 after, spray into spray In the first vapor film 5-6 of quick-fried formula steam engine 5-3, high pressure spray water is successively at spraying-exploding type steam engine 5-3 Each layer vapor film in be heated, very fast be converted into steam；Steam is from the 8th steam of spraying-exploding type steam engine 5-3 Layer 5-18 is out, enter in gas-distributing cylinder 5-21 through vapor film outlet conduit 5-20；Solid material and liquid Raw material from feeding-in solid body tank 1-4 and liquid feedstock tank 1-3 enter in material thermal decomposition pipe 1-2 (quantity of steam is many, Material amount is few), by high-temperature steam carry it into material thermal decomposition pipe 1-2 tube side in carry out head-on collision decompose, Concentrate, be dried, expanded, and readily penetrate through material, the moisture in material become steam, enters back into horizontal Sub-argument device 2-2 or rotation sub-argument tower 2-1:
A) horizontal sub-argument device 2-2 plays, equipped with cooling water layer 2-2-3, the effect of cooling, and the second product is received Collection tank 2-2-6 and dividing plate 2-2-1 is deposited in the second different products the material of different specific weight in raw material and collects In tank 2-2-6, the water in cooling water layer 2-2-3 is in charge of 6-8 and second cooling by the second cooling water water inlet Water backwater is in charge of 6-11 and is circulated in cooling tower 3-1 and cooling water layer 2-2-3, plays the horizontal sub-argument of cooling The effect of device 2-2；Rotate sub-argument tower 2-1 and play, equipped with the first cooling water layer 2-1-6, the effect of cooling, First product collecting tank 2-1-10 and deflection plate 2-1-4 is deposited in the material of condensation temperatures different in raw material In the first different product collecting tank 2-1-10, the water in cooling water layer 2-1-6 is entered by the first cooling water Moisture pipe 6-7 and first cooling water backwater is in charge of 6-10 and is circulated in cooling tower 3-1 and first cooling water layer In 2-1-6, play cooling and rotate the effect of sub-argument tower 2-1.
B) head-on collision of the steam in horizontal sub-argument device 2-2 raw material moves in horizontal sub-argument device 2-2 and floats, By the cooling water layer 2-2-3 effect of being cooled, it is achieved cool reduction, in different distances the most on year-on-year basis Weight raw material falls in the second different product collecting tank 2-2-6.
The steam head-on collision raw material rotated in sub-argument tower 2-1 moves, by rotary tank in rotating sub-argument tower 2-1 2-1-1 effect, mummification solid material directly sinks to rotate particulate matter product collecting tank below sub-argument tower 2-1 In 2-1-9, Gaseous materials rises to rotate in sub-argument tower 2-1 and is cooled work by cooling down water layer 2-1-6 With, it is achieved cool reduction, falls into the first different products at different distance difference condensation temperature raw materials In collecting tank 2-1-10.
Breach steam boiler steam multistage with steam head-on collision material thermal decomposition sub-argument device to concentrate, steam The traditional handicraft sent out, dry, its advantage is the composition according to different material solution, can use different high temperature Steam carries out that head-on collision concentrates, evaporates, dry regulation makes material separate.Material decomposition rate is fast, high-temperature steam Penetration capacity strong (similar Traditional paint spray technique), can be collected according to material different quality.Equipment letter Easily, cost of investment is low.This utility model Product Green environmental protection, safe, energy-conservation, a tractor serves several purposes, can be used for Concentration, distillation, mummification, extract, any technique of refining can be applied in sewage, Treatment of Sludge, life Garbage disposal, veterinary antibiotics drying and other treatment, veterinary antibiotics natural juice refine, acid purification, feed manufacturing, Sugar purification processing, ethanol purification processing, Spirit, mineral classification processing, petrochemical industry refinement, Pharmaceutical Purification, distillation technique, garbage extract nutrient substance, utility collection etc. and uses the industry of heat exchange It is integrated that production carries out technique.
Of the present utility model it is embodied as:
Material of the present utility model processes and includes that liquid processes, liquid-solid mixture matter processes and solid matter Process:
1. liquid processes:
Liquid is processed as percolate sewage disposal, and percolate is a kind of its Mineral work of high-concentration sewage The technique such as industry, treatment of urban garbage has the sewage of high toxicity, high concentration；The most general employing heats combustion Burning into row process, not only processing cost length high, time-consuming can't extract the useful component in percolate；Material It is solid when high temperature that thermal decomposition sub-argument device takes entrance thermal decomposition system 1 to carry out solid-liquid resolution process Liquid is the most separable, and solid matter carries out utility extraction, liquid after feeding-in solid body tank 1-4 collects It is changing into water and carries out sub-argument in material sub-argument system 2, wherein have the element that liquid quality is big rotating sub-argument The liquid that carries out of each different parts in tower 2-1 concentrates collection, and water formation gas after-purification condensation is reclaimed, Mining industry, ethanol manufacturing industry, starch manufacturing industry can be processed according to using material thermal decomposition sub-argument device to process Concentration and collection Deng the process with wherein material concentrating sewage.
2. liquid-solid mixture matter processes:
1) sludge drying processes
Sludge drying processes and the most typically uses nature mummification, heating power mummification, high level cadre's dewatering process to carry out mummification, Process implementing energy consumption is big, time length, the most；Use material thermal decomposition sub-argument device to process to be put into by mud Thermal decomposition system 1 thermally decomposes, is re-fed into rotating sub-argument tower 2-1 and makes the thorough mummification of mud, after mummification Mud collect in particulate matter product collecting tank 2-1-9, wherein liquid part enter rotate sub-argument tower carry out Sub-argument, wherein has the first product of element that liquid quality is big each different parts in rotating sub-argument tower to receive Collection tank 2-1-10 is collected, and water formation gas after-purification condensation is reclaimed.The method can also replace respectively Kind need material thermal decomposition, the multistage evaporation of hot sub-argument, distill, the technological process such as extraction.
2) vegetable drying and other treatment
Vegetable mummification is a various pickled vegetable processing technology needing holding time length to carry out, the ripest bubble face etc. The vegetable needed, the power consumption of current processing technique is greatly；Time is the longest；Artificial the most and operative is different The most arduous, use material thermal decomposition sub-argument device process to be put into by vegetable and thermal decomposition system 1 carries out heat point Solving, be re-fed into rotating sub-argument tower 2-1 and make the thorough mummification of vegetable, the vegetable after mummification is collected at particulate matter product Collecting in tank 2-1-9, wherein liquid part entrance rotation sub-argument tower 2-1 carries out sub-argument, wherein has liquid matter The the first product collecting tank 2-1-10 measuring the big element each different parts in rotating sub-argument tower 2-1 enters Row is collected, and water formation gas after-purification condensation is reclaimed.
3. solid matter processes:
1) Ore such as lead, stannum refines
The ore dressing of the Ore such as lead, stannum is currently pyrometallurgical smelting and electrolytic separation, at the process energy such as roasting, sintering The disadvantages such as consumption is big, choosing point is incomplete can not solve always, uses material thermal decomposition sub-argument device to process Ore It is processed in certain purpose process material input thermal decomposition system 1 and thermally decomposes, be re-fed into horizontal sub-argument dress Putting 2-2 and make thorough mummification, the Ore after mummification enters horizontal sub-argument device and carries out sub-argument, the most various mineral Matter is according to different the second product collecting tank of different parts in horizontal sub-argument device 2-2 respectively of its quality 2-2-6 collects.
2) other
Material thermal decomposition, sub-argument is used under conditions of heat-conducting medium reaches to meet various mineral melting temperature Device can carry out refinement and the extraction of various mineral.

Claims (6)

1. material thermal decomposition sub-argument device, it is characterized in that, be made up of thermal decomposition system (1), material sub-argument system (2), UTILIZATION OF VESIDUAL HEAT IN emission treatment systems (3), heating system (4), steam generating system (5)；
1) thermal decomposition system:
1.1) structure of thermal decomposition system:
Described thermal decomposition system (1) is made up of heat-conducting medium pipe (1-1), material thermal decomposition pipe (1-2), liquid feedstock tank (1-3), feeding-in solid body tank (1-4), Solid Conveying and Melting device (1-5), liquid feed pipe (1-6) and feeding-in solid body pipe (1-7)；
Described heat-conducting medium pipe (1-1) and material thermal decomposition pipe (1-2) are double-tube heat exchanger, are externally provided with heat-insulation layer, and set outer tube layer is heat-conducting medium pipe (1-1), and internal layer is material thermal decomposition pipe (1-2)；Being heat-conducting medium in described heat-conducting medium pipe (1-1), heat-conducting medium is conduction oil or fuse salt；It is mixed material to be thermally decomposed and steam in described material thermal decomposition pipe (1-2)；
Described liquid feedstock tank (1-3) is slack tank body, the built-in liquid material that need to decompose；
Described feeding-in solid body tank (1-4) is slack tank body, the built-in solid particle material that need to decompose；
1.2) annexation of thermal decomposition various parts:
Gas-distributing cylinder (5-21) is connected with the A12 end of jet chimney (6-18), the B12 end of jet chimney (6-18) is connected with the outlet of liquid feedstock tank (1-3) and Solid Conveying and Melting device (1-5), it is connected with the import of material thermal decomposition pipe (1-2) at the B12 end of jet chimney (6-18) the most again, the import of Solid Conveying and Melting device (1-5) is connected with the outlet of feeding-in solid body tank (1-4), liquid feed pipe (1-6) is installed in liquid feedstock tank (1-3) front end, feeding-in solid body pipe (1-7) is installed in feeding-in solid body tank (1-4) front end, the outlet of material thermal decomposition pipe (1-2) is connected with the A1 of mixed material outlet conduit (6-1)；
Described heat-conducting medium pipe (1-1) import is connected with the B13 end of heat-conducting medium conduit (6-19), heat-conducting medium pipe (1-1) outlet is connected with the A14 end of heat-conducting medium outlet conduit (6-20), and heat-conducting medium outlet conduit (6-20) is connected with the heating coil (4-2) of heating system (4) constant temperature oven (4-1) at B14 end by heat-conducting medium circulating pump (7-3)；
2) material sub-argument system:
2.1) structure of material sub-argument system:
The structure of described material sub-argument system is by rotating sub-argument tower (2-1) or horizontal sub-argument device (2-2) forms；
null2.1.1) described rotation sub-argument tower (2-1) bottom is in funnel shaped rotary tank (2-1-1)，Particulate matter product collecting tank (2-1-9) is had at rotary tank，More than tower bottom in cylindrical shape，Tower wall more than tower inner bottom part is from bottom to up for the multiple structure repeated、It is uniformly provided with convection current water interlayer (2-1-2)，It is arranged above with overflow pipe (2-1-3) at convection current water interlayer，In the middle of tower, every layer of convection current water interlayer (2-1-2) is arranged over deflection plate (2-1-4)，Tower outer wall is provided with cooling water layer (2-1-6)，It is provided with condensate water guide sheet (2-1-5) in first cooling water layer (2-1-6)，Tower top is respectively equipped with the first explosion proof door (2-1-7) and the first inspection manhole (2-1-8)，It is provided with the first product collecting tank (2-1-10) in the lower section of outer every layer of convection current water interlayer (2-1-2) position of tower；
2.1.2) described horizontal sub-argument device (2-2) is bullet, pre-small post-large, device inwall is equipped with dividing plate (2-2-1), there is cooling water flow deflector (2-2-2) outside in having the second cooling water layer (2-2-3), the second cooling water layer (2-2-3), is provided with the second product collecting tank (2-2-6), tail end is provided with the second explosion proof door (2-2-4) and the second inspection manhole (2-2-5) below device；
2.1.3) the first mixed material outlet subtube (6-2) and the second mixed material outlet subtube (6-3) in the material sub-argument system described in are two constant section ducts that mixed material outlet conduit (6-1) separates, on first mixed material outlet subtube (6-2), the first valve (6-4) is installed, on second mixed material outlet subtube (6-3), the second valve (6-5) is installed, first valve (6-4) plays effect that is different according to combustion and that select horizontal sub-argument device (2-2) or rotation sub-argument tower (2-1) to carry out material sub-argument with the second valve (6-5)；
2.2) annexation of material sub-argument various parts:
2.2.1) inlet tube and the first cooling water of the first cooling water layer (2-1-6) of described rotation sub-argument tower (2-1) is intake and is in charge of the B3 end connection of (6-7), and the outlet of the first cooling water layer (2-1-6) of rotation sub-argument tower (2-1) and the first cooling water backwater are in charge of the A6 end connection of (6-10)；The B1 end of the import and the first mixed material outlet subtube (6-2) that rotate sub-argument tower (2-1) is connected；
2.2.2) inlet tube and the second cooling water of the second cooling water layer (2-2-3) of described horizontal sub-argument device (2-2) is intake and is in charge of the B4 end connection of (6-8), and the outlet of the second cooling water layer (2-1-6) of horizontal sub-argument device (2-2) and the second cooling water backwater are in charge of the A7 end of (6-11) and are connected；The import of horizontal sub-argument device (2-2) is connected with the B2 end of the second mixed material outlet subtube (6-3)；
3) UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
3.1) structure of UTILIZATION OF VESIDUAL HEAT IN emission treatment systems:
Described UTILIZATION OF VESIDUAL HEAT IN emission treatment systems (3) is mainly made up of cooling tower (3-1), cooling tower water inlet pipe (3-2), hot water swap tank (3-3) and desulfation dust-extraction device (3-7)；
Described cooling tower (3-1) is slack tank body；Described hot water swap tank (3-3) is slack tank body, and the built-in water of tank is also provided with waste heat coil pipe (3-4)；
3.2) annexation of UTILIZATION OF VESIDUAL HEAT IN emission treatment systems (3) each parts:
Described cooling tower (3-1) is connected with hot water swap tank (3-3) by conducting water inlet pipe (3-9), the A15 end of conducting water inlet pipe (3-9) is connected with the import of cooling tower (3-1), and the B15 end of conducting water inlet pipe (3-9) is connected with the import of hot water swap tank (3-3)；The outlet and second of the water inlet of cooling tower (3-1) is in charge of the A6 end of (6-10) respectively by the B7 end of CWR (6-9) with the first cooling water backwater and the second cooling water backwater is in charge of (6-11) A7 end and the first cooling water layer (2-1-6) cools down water layer (2-2-3) outlet and is connected；
The outlet of cooling tower (3-1) is in charge of the B3 end of (6-7) respectively by cooling water circulating pump (7-1) and cooling water inlet pipe (6-6) with the first cooling water water inlet and the second cooling water water inlet is in charge of the B4 end of (6-8) and is cooled down water layer (2-2-3) water inlet with the first water inlet cooling down water layer (2-1-6) and second and be connected；
Described waste heat coil pipe (3-4) lower end exports with the flue (4-3) of heating system (4) and is connected；The outlet of described waste heat coil pipe (3-4) is connected with the import of desulfation dust-extraction device (3-7), and the outlet of desulfation dust-extraction device (3-7) is connected with the import of air-introduced machine (3-5)；The water inlet of desulfation dust-extraction device (3-7) is connected with water inlet pipe (3-8), the mixture outlet of desulfation dust-extraction device (3-7) is connected with the import of liquid feedstock tank (1-3) by blow-off pipe (6-16)；
4) heating system:
4.1) structure of heating system:
Described heating system (4) is made up of constant temperature oven (4-1), heating coil (4-2), cigarette logical (4-3), low level heat-conducting medium storage tank (4-4) and high-order heat-conducting medium expansion slot (4-5)；
Described constant temperature oven (4-1) is heated at constant temperature body of heater, has heat-insulation layer outside body of heater, interior for heating chamber, is provided with the heating coil (4-2) of band heat-conducting medium import and export pipe in heating chamber；
4.2) annexation of each parts of heating system:
2) annexation of each parts of heating system:
The outlet of described high-order heat-conducting medium expansion slot (4-5) is connected with the import of low level heat-conducting medium storage tank (4-4)；The outlet of described low level heat-conducting medium storage tank (4-4) is connected with the first heat-conducting medium layer (5-5) of steam generating system (5) by the B11 end of heat-conducting medium inlet tube (6-17)；The outlet of described heating coil (4-2) is connected with the outlet of low level heat-conducting medium storage tank (4-4) after being connected with the A11 end of heat-conducting medium inlet tube (6-17)；The import of described heating coil (4-2) is connected with the B14 end of heat-conducting medium outlet conduit (6-20), and the A14 end of heat-conducting medium outlet conduit (6-20) is connected with the outlet of the heat-conducting medium conduit (1-1) of thermal decomposition system (1)；The import of heat-conducting medium conduit (1-1) is connected with the outlet of the 8th heat-conducting medium layer (5-19) of steam generating system (5)；Heat-conducting medium circulating pump (7-3) is had on heat-conducting medium outlet conduit (6-20)；
5) steam generating system
5.1) structure of steam generating system:
Described steam generating system (5) is mainly made up of high-pressure plunger pump (5-1), spraying-exploding type steam engine (5-3), high pressure sprays fog equipment (5-4), gas-distributing cylinder (5-21) and relief valve (5-22)；
nullThe multilamellar ring-type sealing ring road of heat-insulation layer is had outside described spraying-exploding type steam engine (5-3)，It is the first heat-conducting medium layer (5-5) respectively、Second heat-conducting medium layer (5-7)、3rd heat-conducting medium layer (5-9)、4th heat-conducting medium layer (5-11)、5th heat-conducting medium layer (5-13)、6th heat-conducting medium layer (5-15)、7th heat-conducting medium layer (5-17) and the 8th heat-conducting medium layer (5-19)，First vapor film (5-6)、Second vapor film (5-8)、3rd vapor film (5-10)、4th vapor film (5-12)、5th vapor film (5-14)、6th vapor film (5-16) and the 7th vapor film (5-18)，First vapor film (5-6) and the second vapor film (5-8)、Second vapor film (5-8) and the 3rd vapor film (5-10)、3rd vapor film (5-10) and the 4th vapor film (5-12)、4th vapor film (5-12) and the 5th vapor film (5-14)、5th vapor film (5-14) and the 6th vapor film (5-16)、6th vapor film (5-16) and the 7th vapor film (5-18) are respectively equipped with communicating pipe，First heat-conducting medium layer (5-5) and the second heat-conducting medium layer (5-7)、Second heat-conducting medium layer (5-7) and the 3rd heat-conducting medium layer (5-9)、3rd heat-conducting medium layer (5-9) and the 4th heat-conducting medium layer (5-11)、4th heat-conducting medium layer (5-11) and the 5th heat-conducting medium layer (5-13)、5th heat-conducting medium layer (5-13) and the 6th heat-conducting medium layer (5-15)、6th heat-conducting medium layer (5-15) and the 7th heat-conducting medium layer (5-17)、7th heat-conducting medium layer (5-17) and the 8th heat-conducting medium layer (5-19) are respectively equipped with communicating pipe；
5.2) annexation of each parts of steam generating system:
7th vapor film (5-18) outlet of the spraying-exploding type steam engine (5-3) in described steam generating system (5) is connected by the import of vapor film outlet conduit (5-20) with gas-distributing cylinder (5-21)；
8th heat-conducting medium layer (5-19) outlet of described spraying-exploding type steam engine (5-3) is connected with the A13 end of heat-conducting medium conduit (6-19)；
The outlet of described gas-distributing cylinder (5-21) is connected with the A12 end of jet chimney (6-18), and the B12 end of jet chimney (6-18) is connected with the import of material thermal decomposition pipe (1-2)；
Described high-pressure plunger pump (5-1) import is connected with the water out of hot water swap tank (3-3)；High-pressure plunger pump (5-1) outlet is connected with high pressure sprays fog equipment (5-4) by high-pressure plunger pump discharge pipe (5-2)；
Relief valve (5-22) is installed on described gas-distributing cylinder (5-21).
Material the most according to claim 1 thermal decomposition sub-argument device, it is characterised in that described spraying-exploding type steam engine (5-3) its act as atomizing heated moisture body, be 1～1000 spraying-exploding type steam engine parallel combination body.
Material the most according to claim 1 thermal decomposition sub-argument device, it is characterised in that described constant temperature oven (4-1) is 1～100 constant temperature oven parallel combination body.
Material the most according to claim 1 thermal decomposition sub-argument device, it is characterised in that described rotation sub-argument tower (2-1) in material sub-argument system (2) and horizontal sub-argument device (2-2) are assemblys that can be jointly in parallel.
Material the most according to claim 1 thermal decomposition sub-argument device, it is characterised in that more than rotation sub-argument tower (2-1) interior bottom portion in described material sub-argument system (2) be the multiple structure repeated from bottom to up, be 1～100 layer.
Material the most according to claim 1 thermal decomposition sub-argument device, it is characterised in that the horizontal sub-argument device (2-2) in described material sub-argument system (2) is internal is from first to last the many diaphragm structures repeated, and is 1～100 piece of dividing plate.
CN201620022569.2U 2016-01-11 2016-01-11 Material thermolysis divides reason device Withdrawn - After Issue CN205634946U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105481037A (en) * 2016-01-11 2016-04-13 赖正平 Substance thermal decomposition and sub-treatment device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105481037A (en) * 2016-01-11 2016-04-13 赖正平 Substance thermal decomposition and sub-treatment device

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